Preparation of microporous chlorinated poly(vinyl chloride) membrane in fabric and the characterization of their pore sizes and pore-size distributions

2002 ◽  
Vol 86 (5) ◽  
pp. 1195-1202 ◽  
Author(s):  
Jong Seok Kang ◽  
Ki Yoen Kim ◽  
Young Moo Lee
2020 ◽  
Author(s):  
Scott C. Hauswirth ◽  
◽  
Majdi Abou Najm ◽  
Christelle Basset

SPE Journal ◽  
2015 ◽  
Vol 20 (04) ◽  
pp. 824-830 ◽  
Author(s):  
Richard F. Sigal

Summary The behavior of fluids in nanometer-scale pores can have a strong functional dependence on the pore size. In mature organic-shale reservoirs, the nuclear-magnetic-resonance (NMR) signal from methane decays by surface relaxation. The methane NMR spectrum provides an uncalibrated pore-size distribution for the pores that store methane. The distribution can be calibrated by calculating a pore-wall-surface area from a methane-Langmuir-adsorption isotherm. When this method was applied to samples from a reservoir in the dry-gas window, the pores containing methane had pore sizes that ranged from 1 to approximately 100 nm. Approximately 20–40% of the pore volume was in pores smaller than 10 nm, where deviation from bulk-fluid behavior can be significant. The samples came from two wells. The surface relaxivity for the sample from Well 2 was somewhat different from the relaxivity for the two samples from Well 1. Samples that adsorbed more methane had smaller pore sizes. This methodology to obtain pore-size distributions should be extendable to more-general organic-shale reservoirs.


2019 ◽  
Vol 6 (3) ◽  
pp. 28-36
Author(s):  
Çiğdem Akduman

Cellulose acetate (CA) nanofiber membranes incorporated with diatomite (DE) were prepared by electrospinning to produce electrospun nanofiber membranes with high specific surface area and high porosity with fine pores. When the DE percentage increased from 0 to 30%, the water contact angle (WCA) of the membranes increased from 86.21° to 118.44°, indicating that neat CA nanofibers were more hydrophilic than CA/DE nanofibers and had a better wetting tendency. CA, CA-10DE, and CA-20DE nanofiber membranes showed a mean flow pore size (MFP) of 2.941, 2.681, and 2.408 μm, respectively, with narrow pore size distributions. However, the CA-30DE nanofiber membrane showed a smaller MFP size of 0.5014 μm. CA nanofibers were produced in the range of 206.31 to 281.13 nm. The dye removal ability of these membranes was tested using an aqueous solution of C.I. Reactive Red 141.


2016 ◽  
Vol 48 (2) ◽  
pp. 106-114 ◽  
Author(s):  
Joko Sampurno ◽  
◽  
Azrul Azwar ◽  
Fourier Dzar Eljabbar Latief ◽  
Wahyu Srigutomo ◽  
...  

2016 ◽  
Vol 48 (2) ◽  
pp. 106-114
Author(s):  
Joko Sampurno ◽  
◽  
Azrul Azwar ◽  
Fourier Dzar Eljabbar Latief ◽  
Wahyu Srigutomo ◽  
...  

2021 ◽  
Author(s):  
Martin Lanzendörfer

<p>Following the capillary bundle concept, i.e. idealizing the flow in a saturated porous media in a given direction as the Hagen-Poiseuille flow through a number of tubular capillaries, one can very easily solve what we would call the <em>forward problem</em>: Given the number and geometry of the capillaries (in particular, given the pore size distribution), the rheology of the fluid and the hydraulic gradient, to determine the resulting flux. With a Newtonian fluid, the flux would follow the linear Darcy law and the porous media would then be represented by one constant only (the permeability), while materials with very different pore size distributions can have identical permeability. With a non-Newtonian fluid, however, the flux resulting from the forward problem (while still easy to solve) depends in a more complicated nonlinear way upon the pore sizes. This has allowed researchers to try to solve the much more complicated <em>inverse problem</em>: Given the fluxes corresponding to a set of non-Newtonian rheologies and/or hydraulic gradients, to identify the geometry of the capillaries (say, the effective pore size distribution).</p><p>The potential applications are many. However, the inverse problem is, as they usually are, much more complicated. We will try to comment on some of the challenges that hinder our way forward. Some sets of experimental data may not reveal any information about the pore sizes. Some data may lead to numerically ill-posed problems. Different effective pore size distributions correspond to the same data set. Some resulting pore sizes may be misleading. We do not know how the measurement error affects the inverse problem results. How to plan an optimal set of experiments? Not speaking about the important question, how are the observed effective pore sizes related to other notions of pore size distribution.</p><p>All of the above issues can be addressed (at least initially) with artificial data, obtained e.g. by solving the forward problem numerically or by computing the flow through other idealized pore geometries. Apart from illustrating the above issues, we focus on <em>two distinct aspects of the inverse problem</em>, that should be regarded separately. First: given the forward problem with <em>N</em> distinct pore sizes, how do different algorithms and/or different sets of experiments perform in identifying them? Second: given the forward problem with a smooth continuous pore size distribution (or, with the number of pore sizes greater than <em>N</em>), how should an optimal representation by <em>N</em> effective pore sizes be defined, regardless of the method necessary to find them?</p>


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